CFD simulation of a pilot scale slurry photocatalytic reactor and design of multiple-lamp reactors

被引:37
作者
Boyjoo, Yash [1 ]
Ang, Ming [1 ]
Pareek, Vishnu [1 ]
机构
[1] Curtin Univ, Dept Chem Engn, Perth, WA 6102, Australia
关键词
Photocatalytic; Radiation; Multi-lamps; Multiphase; Modelling; LIGHT-INTENSITY DISTRIBUTION; BUBBLE-COLUMN; NUMERICAL-SIMULATION; RADIATION-FIELD; DYNAMICS; MODEL; DEGRADATION; SCATTERING; PARTICLES; OXIDATION;
D O I
10.1016/j.ces.2014.02.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The hydrodynamics behaviour and radiation transport occurring inside a pilot-scale slurry photocatalytic reactor (treating real shower water) with large diameter was investigated using computational fluid dynamics (CM). The multiphase flow system was solved using a granular Eulerian model while the solution of the radiative transport equation (RTE) was solved using the finite volume based discrete ordinate model (DOM). Multiphase simulation showed recirculation zones caused by the high slurry inlet velocity. Due to the rapid attenuation of light occurring radially within the reactor, regions of varying reaction orders exist, i.e., half order reaction close to the lamp and first order reaction further from the lamp, as the incident radiation goes below a certain value. A rate equation relating pollutant degradation to the rate occurring in the half and first order reaction regions (in terms of local volumetric rate of energy absorption - LVREA) was proposed. Using a value of 225W m(-2) as the minimum incident light intensity at which half order reactions take place, a Pearson correlation of 0.88 between simulated and experimental data indicated that the proposed model satisfactorily described the experimental observations. Next, simulations performed with a system of multiple lamps (2 and 4 lamps) at different geometrical arrangements (i.e. with the lamps separated by the distance X-lamp) showed that within the range of catalyst concentration investigated, the maximum potential increases in reaction rate was 56% and 123% when using 2 and 4 lamps (at optimum lamp arrangement) respectively, as compared to using one lamp. The increase in reaction rate occurred due to the maximisation of incident radiation contours at which first order reactions Lake place. The optimum lamp separation was dependent on the catalyst concentration in the wastewater and decreased with increasing catalyst concentration. (C) 2014 Elsevier Ltd. All rights reserved
引用
收藏
页码:266 / 277
页数:12
相关论文
共 45 条
  • [1] 2-D radiation field in photocatalytic channels of square, rectangular, equilateral triangular and isosceles triangular sections
    Alexiadis, A
    [J]. CHEMICAL ENGINEERING SCIENCE, 2006, 61 (02) : 516 - 525
  • [2] [Anonymous], 2011, IN MAT CAT INN AEROS
  • [3] Boyjoo Y., 2013, THESIS CURTIN U
  • [4] Boyjoo Y., 2012, INT J PHOTOENERGY, V2012, P7
  • [5] Some aspects of photocatalytic reactor modeling using computational fluid dynamics
    Boyjoo, Yash
    Ang, Ming
    Pareek, Vishnu
    [J]. CHEMICAL ENGINEERING SCIENCE, 2013, 101 : 764 - 784
  • [6] Light intensity distribution in multi-lamp photocatalytic reactors
    Boyjoo, Yash
    Ang, Ming
    Pareek, Vishnu
    [J]. CHEMICAL ENGINEERING SCIENCE, 2013, 93 : 11 - 21
  • [7] Eulerian-Lagrangian simulations of unsteady gas-liquid flows in bubble columns
    Buwa, Vivek V.
    Deo, Dhanannjay S.
    Ranade, Vivek V.
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2006, 32 (07) : 864 - 885
  • [8] Reaction engineering of suspended solid heterogeneous photocatalytic reactors
    Cassano, AE
    Alfano, OM
    [J]. CATALYSIS TODAY, 2000, 58 (2-3) : 167 - 197
  • [9] Determination of kinetic constants of a photocatalytic reaction in micro-channel reactors in the presence of mass-transfer limitation and axial dispersion
    Charles, Guillaume
    Roques-Carmes, Thibault
    Becheikh, Nidhal
    Falk, Laurent
    Commenge, Jean-Marc
    Corbel, Serge
    [J]. JOURNAL OF PHOTOCHEMISTRY AND PHOTOBIOLOGY A-CHEMISTRY, 2011, 223 (2-3) : 202 - 211
  • [10] Simulations of Photodegradation of Toluene and Formaldehyde in a Monolith Reactor Using Computational Fluid Dynamics
    Chong, Siewhui
    Wang, Shaobin
    Tade, Moses
    Ang, H. Ming
    Pareek, Vishnu
    [J]. AICHE JOURNAL, 2011, 57 (03) : 724 - 734